In-Process Device and Method for Cell Culture Monitoring
20220081671 · 2022-03-17
Inventors
- Swapnil Puranik (Bengaluru, Karnataka, IN)
- Manoj Kumar Ramakrishna (Bengaluru, Karnataka, IN)
- Haresh Patil (Bengaluru, Karnataka, IN)
Cpc classification
C12M41/46
CHEMISTRY; METALLURGY
International classification
C12M1/34
CHEMISTRY; METALLURGY
C12M3/06
CHEMISTRY; METALLURGY
Abstract
Disclosed is an in-process cell monitoring device comprising: a flow channel having at least one inlet and at least one outlet exposeable to a cell culture; a microscope positionable to view the contents of a region of the channel; and a computer operable at least to count any cells in the region, providing a closed fluid circuit for cell monitoring. Disclosed also is a bioreactor including a cell culture volume, and an in-process cell monitoring device, said device comprising: a flow channel having at least one inlet and at least one outlet each in fluid communication with the volume, of sufficient cross-sectional area to allow fluids to drain from the inlet to the outlet; and a microscope positionable to view the contents of a region of the channel, and also A method for monitoring a cell culture including determining cell density.
Claims
1. An in-process cell monitoring device comprising: a monitoring flow channel having at least one inlet and at least one outlet exposeable to a cell culture; a microscope positionable to view the contents of a region of the channel; and a computer operable at least to count any cells in the region.
2. The device as claimed in claim 1, wherein the flow channel is illuminated.
3. The device as claimed in claim 1, wherein the flow channel, at least at said region, is transparent or translucent, and is a closed channel other than said inlet and outlet.
4. The device as claimed in claim 1, wherein the flow channel is self draining and optionally includes no pools or dead ends or areas of fluid stagnation.
5. The device as claimed in claim 1, wherein the flow channel at the region has a depth, in the direction of viewing, of about 1 mm to about 3 mm, which is a uniform depth over the viewing region area.
6. The device as claimed in claim 1, wherein the flow channel has a substantially uniform cross sectional area, or has a uniformly tapering cross sectional area at the region and optionally is increased in cross section area at the inlet and optionally at the outlet also.
7. The device as claimed in claim 1, wherein said at least one inlet and at least one outlet comprises two inlets and two outlets.
8. A bioreactor including a cell culture volume, and an in-process cell monitoring device, said device comprising: a flow channel having at least one inlet and at least one outlet each in fluid communication with the volume, of sufficient cross-sectional area to allow fluids to drain from the inlet to the outlet; and a microscope positionable to view the contents of a region of the channel.
9. The bioreactor as claimed in claim 8, wherein at least a majority of said channel is disposed within the culture volume, and said microscope is releasably held to the remaining device externally of said volume.
10. The cell culture apparatus including a bioreactor as claimed in claim 8, said apparatus further including a bioreactor mover, moveable with sufficient magnitude as to cause a portion of any fluid in the bioreactor to flow through the flow channel.
11. A method for monitoring a cell culture including determining cell density comprising, in any suitable order, the following steps: a) causing a flow of fluid through a region of a monitoring channel of predetermined cross-sectional area; b) capturing an image of the region; c) using a computer, determining the number of cells imaged for a predetermined time; d) using data from more than one image, determining the flow speed through measuring channel; e) using the determined flow speed and cross-sectional area at the region, determining the volumetric flow rate in the channel; and f) determining the cell density from said number of cells imaged and the volumetric flow rate.
12. The method of claim 11, wherein the step of determining the speed of flow includes analysis of successive captured cell images at known time intervals and/or the step of determining the volumetric flow rate includes multiplying the speed of flow by the cross-sectional area.
13. The method of claim 11, including the further step of determining the viability of the cells imaged, by means of assigning a light density value to successive pixels from a captured image, and determining the rate of change of the light density value of a cell wall area.
14. The method of claim 11, wherein the flow of fluid in step a) is the result is agitating a bioreactor vessel, for example tilting of the said bioreactor vessel.
15. The method of claim 14, wherein said fluid in said flow is substantially drained or exchanged with other fluid after each cycle of agitation, for example after each tilt or after a single figure number of tilts.
Description
DRAWINGS
[0009] The invention will now be described in more detail with reference to the appended drawings, wherein:
[0010]
[0011]
[0012]
[0013]
[0014]
DETAILED DESCRIPTION
[0015]
[0016] The cell culture mix 14 is monitorable by the monitoring device 100, which in this case is attached to the outside of the bag 12, and has an inlet and outlet, described in more detail below, in fluid communication with the interior of the bag 12 and, consequently, the cell culture mix 14. The device 100 further includes an umbilical 102 which includes, in this embodiment an electrical power supply, and signal lines (electrical and/or optical fibre).
[0017] The base 18 includes a complementary a microcontroller and associated hardware 20 for controlling the electrical supply to the device, as well as a data memory for buffering data coming from the device 100, all connected to the device via a complementary umbilical 22, and a connector 24 which mates with a complementary connector 104 on the end of the device's umbilical 102. In summary, the microcontroller is used to control the functioning of the device, and to receive data from the device. Whilst the microcontroller and its associated hardware 20 are preferably located in the base 18, they may be located elsewhere. The complementary connectors 24/104 are used for ease of assembly.
[0018]
[0019] In use, the flow channel 122 is exposed to the culture mix 14, such that fluids, including cells can flow in the direction of arrows F through the channel 122. The cap 120 is formed from a transparent or translucent material, for example a PMMA plastics, such as acrylic plastics, and includes a partially spherical portion 128 which faces the microscope 110, which in turn has the effect of focusing light at a central region 130 of the channel 122, such that light emitted from an LED 112 of the microscope 110, is focused at the focal point region 130, and light emitted from that focal point is captured at an image array 114, in the microscope 110.
[0020] The base 140 includes an internal thread 146, which accepts a complimentary thread 126 formed on an outer surface of the microscope 110. Thus, rotation of the microscope about an axis a relative to the base 140 can adjust the position of the focal point region 130.
[0021] The cap 120, which may be in two halves to make the formation of the channel 122 easier, and the base 140 are intended to form an assembly along with the flexible bag 12. Since the assembly is intended to be disposable, then a removable microscope 110 is preferred in order that the microscope can be reused. So, whilst complimentary threads 126 and 146 have been illustrated, other readily releasable fastening between the base 140 and the microscope 110 could be employed. For example a bayonet fitting or a simple push fit could be employed.
[0022]
[0023]
[0024] It will be understood that other flow path profiles could be employed.
[0025] An alternative cap 520 is shown in
[0026] It will be apparent that the caps shown in
[0027] The cross sectional dimensions of the channels 122, 422, 522 and 622 do not need to be exact however, a depth (X) of 1 to 3 mm has been found to provide reasonably good results. In other words, cells move through such channels under the influence of gravity as the bioreactor bag 12 is rocked back and forth, and travel at a speed which allows them to be imaged. In all cases, the channels have generally parallel top and bottom walls with no regions where fluids can pool or come to a dead end. This means that the fluids in the monitor are constantly flushed and do not stagnate. This is particularly advantageous over existing cell sampling techniques which require drawing off of an aliquot of cell suspension often along a dead end which stagnates and causes a source of atrophy and subsequent contamination. It is important, but not essential to provide a uniform depth (X) of channel across the monitoring region 130 for consistent results. Where the flow becomes choked, for example as will happen in the channel 522 shown in
[0028]
[0029] Image analysis software can be employed to count the number of cells newly appearing in an image, thereby providing a count of the cells over a period of time. The period of time can also be used to determine the total volume of fluids imaged because the cross-sectional area of flow at the image is also known.
[0030] Further, analysis of the images can determine the viability of the cells counted. For example, the inventors have observed that healthy cells have a well-defined cell wall such that an image captured the cells in the channel provides a clear contrast between the cell wall and the fluid suspension. Whereas, a dead or unhealthy cell provides a less distinct contrast. Image analysis of the contrast of the cell in relation to its background can give an indication of the viability of the cell in question. In practice, a light density value can be assigned to successive pixels from the array of the microscope image array 114, and if the rate of change of the density value of a cell wall area is sufficiently large, then that cell can be determined as healthy. Alternatively, where the rate of change of the density value is low then that is an indication that the cell wall is not healthy and that the cell is potentially not viable. Thus, with successive cell image analysis a reasonably accurate determination of cell viability can be obtained, for example as a percentage of the number of cells counted according to the method mentioned above.
[0031] In operation, the cell counting and assessment of cell viability can be performed by computer connected to the microcontroller 20. Such monitoring can be performed continually, periodically, or at random, during the cell culture process, and can be used to influence the parameters of the cell culture, or to determine when the cell density is of sufficient magnitude to end cell culture. This is particularly useful in autologous cell therapies where the characteristics of the seed cells are unknown. Since the channels are simple flat channels with no pockets of fluid that cannot drain away when tilted, then no dead pockets or pools can form, which means that the monitor is self draining and not a source of atrophy or contamination. Thus, it can be seen that the monitoring channel should have sufficient size and shape to allow self-draining of the channel after it is agitated or tilted, although in practice a residue of fluid may remain. However such residue will ultimately be washed away, for example after a low number of cycles, i.e no more than 9 or 10 cycles.
[0032] The monitoring and determination according to the above technique can be repeated multiple times, the cell culture process being monitored by the device and its determinations used to feedback to the controller which can adjust the parameters of the cell culture, for example increasing or decreasing nutrient supply or perfusion rates and determining when the viable cell density has reach the desired levels. Once cell culture is complete, the cell bag 12 and attached device can be discarded, but the microscope can be released and reused with the next bag 12.
[0033] The invention is not to be seen as limited by the embodiments described above, but can be varied within the scope of the appended claims as is readily apparent to the person skilled in the art. For instance, it is preferred that the cap 120 is positioned at the bottom of the cell culture 14, because the cells tend to congregate at the bottom of the suspension fluid. Further, many cell cultures start with a small volume of suspension fluid and increase the fluid volume as culture progresses. Thus, conveniently the cap is positioned at the bottom of the cell culture 14. However, provided that a flow of cells can be made to pass through the channel, then the cap can be positioned anywhere to provide reasonable results. So, in an alternative embodiment, the cap 120 or a similar arrangement including a flow channel can be provided on the end of a probe, which probe can be repositioned within a bioreactor. Such a probe can be inserted into a cell culture vessel, with the microscope preferably remaining outside the vessel. So long as a representative sample of cells is monitored the monitoring channel of the end of the probe which would include a monitoring channel as described above can be positioned anywhere in the vessel.
[0034] In the embodiment illustrated in